EP2255008A2 - Procédé de production de xylitol - Google Patents

Procédé de production de xylitol

Info

Publication number
EP2255008A2
EP2255008A2 EP09722235A EP09722235A EP2255008A2 EP 2255008 A2 EP2255008 A2 EP 2255008A2 EP 09722235 A EP09722235 A EP 09722235A EP 09722235 A EP09722235 A EP 09722235A EP 2255008 A2 EP2255008 A2 EP 2255008A2
Authority
EP
European Patent Office
Prior art keywords
xylose
xylitol
yeast strain
medium
feed solution
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP09722235A
Other languages
German (de)
English (en)
Inventor
Manish Jain
K. V. Satyanarayana
Ashok Kumar Dubey
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tata Chemicals Ltd
Original Assignee
Tata Chemicals Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tata Chemicals Ltd filed Critical Tata Chemicals Ltd
Publication of EP2255008A2 publication Critical patent/EP2255008A2/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P7/00—Preparation of oxygen-containing organic compounds
    • C12P7/02—Preparation of oxygen-containing organic compounds containing a hydroxy group
    • C12P7/04—Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic
    • C12P7/18—Preparation of oxygen-containing organic compounds containing a hydroxy group acyclic polyhydric
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P19/00—Preparation of compounds containing saccharide radicals
    • C12P19/02—Monosaccharides

Definitions

  • the invention relates to the production of xylitol. More particularly the invention relates to the production of xylitol by microbial conversion of xylose in water. DESCRIPTION OF RELATED ART
  • Xylitol is a five-carbon sugar alcohol with significant medical and commercial applications and has been widely used as an alternative low calorie sweetener. Xylitol occurs naturally in many fruits and vegetables and also as a natural intermediate product in glucose metabolism of humans and other animals as well as in the metabolism of several plants and microorganisms.
  • Xylitol has numerous advantages including the same sweetness as sucrose but with one- third fewer calories and no unpleasant aftertaste, hi addition its negative heat of dissolution imparts a cool and refreshing sensation in the oral cavity, making it a popular sweetener for candies and sweets. Xylitol also finds favor with diabetic patients as it is metabolized independently from insulin in the human body. Xylitol has also been shown to have therapeutic properties and reportedly builds immunity, fights against chronic degenerative diseases, is anti- aging, and has no known toxic levels.
  • xylitol In addition to its use in the food, pharmaceutical and oral health products, xylitol also finds commercial applications in plywood industries and can replace phenolic resins because of its adhesive properties.
  • xylitol is produced by chemical reduction of xylose, which is a hydrolysate of hemicellulose present in woods, rice straw, millet, etc.
  • xylitol is produced by chemical reduction of xylose, which is a hydrolysate of hemicellulose present in woods, rice straw, millet, etc.
  • An example of this process is described in the US Patent Number 4008285, in which the production of xylitol on a commercial scale is carried out by acid hydrolysis of pentosan-containing raw materials such as wood, corncobs, straw, bran, and cottonseed hulls.
  • the hydrolysis of xylitol is usually carried out using Raney nickel catalyst (NiZAl 2 O 3 ) at high temperature and pressure.
  • Raney nickel catalyst NiZAl 2 O 3
  • One limitation of the chemical process is the difficulty of separation and purification of xylose or xylitol from hydrolysates of other polymer sugars derived from hemicellulose fractions. Multistep separation techniques, including mechanical filtration and chromatography are required to obtain pure xylitol. These processes adversely affect the cost of production for a yield in the range of 50-60%. Furthermore, such processes involve high temperature and high-pressure associated risks. Waste disposal due to use of acid or alkali is another major concern that is associated with chemical production of xylitol. These factors make the chemical methods for the routine production of xylitol difficult, expensive and inefficient.
  • biotechnological processes have the advantages of selective conversion with high yield and less toxic/nontoxic byproducts where xylose is converted into xylitol by microorganisms using NAD(P)H- dependent xylose reductase (XR).
  • XR NAD(P)H- dependent xylose reductase
  • xylitol from xylose
  • yeast including those of the species Pichia, Candida, Hansenula and Kluyveromyces, are capable of reducing xylose to xylitol as an initial step in their xylose metabolism/bioconversion.
  • the production of xylitol using microorganisms has been carried out by batch, fed batch and cell recycling methods.
  • the cost of microbial production of xylitol depends on a number of factors including the cost of fermentation medium, maintenance of fermentation conditions and cost of recovery of xylitol from the fermentation medium.
  • Microbial methods currently available for the production of xylitol use medium containing xylose along with nutrients that facilitate cell growth. Nutrients that are added are either complex organic compounds like peptone, yeast extract etc. or chemical compounds.
  • the invention relates to a process for producing xylitol from xylose by a yeast strain capable of converting the xylose to xylitol comprising independently growing the yeast strain in a medium; transferring the yeast strain from the medium to a feed solution, the feed solution comprising of xylose in water, and separating the xylitol from said feed solution.
  • the invention relates to a process for producing xylitol from xylose by a yeast strain capable of converting the xylose to xylitol comprising independently growing the yeast strain in a medium; transferring the yeast strain from the medium to a feed solution, the feed solution comprising of xylose in water; recovering the xylitol from said feed solution; and recycling the yeast strain at least once, the recycling comprising transferring the yeast strain to another feed solution; the other feed solution comprising of xylose in water.
  • the invention relates to a process for producing xylitol from xylose by a yeast strain capable of converting the xylose to xylitol comprising growing the yeast strain in a medium including xylose to obtain xylitol; recovering xylitol from medium and transferring the yeast strain from the medium to a feed solution, the feed solution comprising of xylose in water, and separating the xylitol from said feed solution.
  • the invention relates to a process for producing xylitol from xylose by a yeast strain capable of converting the xylose to xylitol comprising growing the yeast strain in a medium including xylose to obtain xylitol; recovering xylitol from medium and transferring the yeast strain from the medium to a feed solution, the feed solution comprising of xylose in water, recovering xylitol from the feed solution and recycling the yeast strain at least once, the recycling comprising transferring the yeast strain to another feed solution; the other feed solution comprising of xylose in water.
  • Figure 1 illustrates shake flask experimental results for xylitol production using C. tropicalis ATCC 13803 at 30 0 C, 250 rpm and pH 6.0.
  • Figure 2 illustrates the experimental results of % Xylitol Production using C. tropicalis ATCC 13803 at 30 0 C, 250 rpm and pH 6.0.
  • Figure 3 illustrates the experimental results of cell recycling experiment for Xylitol Production from Xylose (100 g/L) using C. tropicalis ATCC 13803 at 30 0 C, 215 rpm.
  • Figure 4 Cell recycling experiment for Xylitol Production from Xylose (150 g/L) using C. tropicalis ATCC 13803 at 30 0 C, 215 rpm.
  • the invention provides a method for microbial production of xylitol from a solution of xylose in water. More particularly the invention relates to the production of xylitol from a solution of xylose in water by a yeast strain capable of converting xylose to xylitol.
  • the invention relates to the process of production of xylitol from a solution of xylose in water by yeast wherein the yeast strain is inoculated into a solution of xylose in water to produce xylitol.
  • a process for producing xylitol from xylose by a yeast strain capable of converting the xylose to xylitol is disclosed.
  • the process includes independently growing the yeast strain in a medium and transferring the yeast strain from the medium to a feed solution.
  • the feed solution comprises of xylose in water.
  • Xylitol produced in the feed solution is recovered.
  • the yeast strain is grown independently in a nutrient rich medium, which includes growing the yeast strain in a nutrient rich growth medium till required cell mass is achieved. Yeast cells so grown are separated from the growth medium and transferred to a feed solution of xylose in water.
  • a process for producing xylitol from xylose by a yeast strain capable of converting the xylose to xylitol includes independently growing the yeast strain in a medium and transferring the yeast strain from the medium to a feed solution.
  • the feed solution comprises of xylose in water.
  • Xylitol produced in the feed solution is recovered and the yeast strain is recycled at least once.
  • the recycling comprises transferring the yeast strain to another feed solution that comprises xylose in water.
  • the yeast strain is grown independently in a nutrient rich medium, which includes growing the yeast strain in a nutrient rich growth medium till required cell mass is achieved. Yeast cells so grown are separated from the growth medium and transferred to a feed solution comprising of xylose in water. Xylitol produced is recovered from the feed solution and the yeast strain is recycled at least once by introducing the yeast strain in another feed solution, comprising a solution of xylose in water.
  • a process for producing xylitol from xylose by a yeast strain capable of converting the xylose to xylitol comprising growing the yeast strain in a medium including xylose is disclosed. Xylitol produced is recovered from the medium and the yeast strain is transferred from the medium to a feed solution. The feed solution comprises of xylose in water. Xylitol produced is recovered from the feed solution.
  • the yeast strain is grown independently in a nutrient rich medium including xylose, which includes growing the yeast strain in a nutrient rich growth medium including xylose till required cell mass is achieved. Yeast cells so grown are separated from the growth medium and transferred to a feed solution of xylose in water. Xylitol is recovered from both medium.
  • a process for producing xylitol from xylose by a yeast strain capable of converting the xylose to xylitol comprising growing the yeast strain in a medium including xylose.
  • the process includes growing the yeast strain in a medium including xylose and transferring the yeast strain from the medium to a feed solution.
  • Xylitol produced is recovered from the medium.
  • the feed solution comprises of xylose in water.
  • Xylitol produced in the feed solution is recovered and the yeast strain is recycled at least once.
  • the recycling comprises transferring the yeast strain to another feed solution that comprises of xylose in water.
  • the yeast strain is grown in a nutrient rich medium including xylose, which includes growing the yeast strain in a nutrient rich growth medium till required cell mass is achieved and xylitol is produced.
  • Yeast cells so grown are separated from the medium and transferred to a feed solution of xylose in water.
  • Xylitol produced is recovered from the feed solution and the yeast strain is recycled at least once by introducing the yeast strain in a medium containing a solution of xylose in water.
  • a process for producing xylitol from xylose by a yeast strain capable of converting the xylose to xylitol includes independently growing the yeast strain in a medium to which nutrients are gradually added and transferring the yeast strain from the medium to a feed solution.
  • the feed solution comprises of xylose in water. Xylitol produced in the feed solution is recovered.
  • the yeast strain is grown independently in a nutrient rich medium, in which nutrients are gradually added, which includes growing the yeast strain in a growth medium gradually supplemented by nutrients till required cell mass is achieved. Yeast cells so grown are separated from the growth medium and transferred to a feed solution of xylose in water.
  • a process for producing xylitol from xylose by a yeast strain capable of converting the xylose to xylitol includes independently growing the yeast strain in a medium to which nutrients are gradually added and transferring the yeast strain from the medium to a feed solution.
  • the feed solution comprises of xylose in water.
  • Xylitol produced in the feed solution is recovered and the yeast strain is recycled at least once.
  • the recycling comprises transferring the yeast strain to another feed solution that comprises of xylose in water.
  • the yeast strain is grown independently in a nutrient rich medium, in which nutrients are gradually added, which includes growing the yeast strain in a growth medium gradually supplemented by nutrients till required cell mass is achieved.
  • Yeast cells so grown are separated from the growth medium and transferred to a feed solution of xylose in water.
  • Xylitol produced is recovered from the feed solution and the yeast strain is recycled at least once by introducing the yeast strain in another feed solution that comprises of xylose in water.
  • a process for producing xylitol from xylose by a yeast strain capable of converting the xylose to xylitol comprising growing the yeast strain in a medium including xylose, where nutrients and xylose are gradually added is disclosed.
  • Xylitol produced is recovered from the medium and the yeast strain is transferred from the medium to a feed solution.
  • the feed solution comprises of xylose in water.
  • Xylitol produced is recovered from the feed solution.
  • the yeast strain is grown in a nutrient rich medium, in which nutrients and xylose are gradually added, which includes growing the yeast strain in a growth medium gradually supplemented by nutrients and xylose till required cell mass is achieved.
  • Yeast cells so grown are separated from the medium and transferred to a feed solution of xylose in water. Xylitol is recovered from both mediums.
  • a process for producing xylitol from xylose by a yeast strain capable of converting the xylose to xylitol comprising growing the yeast strain in a medium including xylose where nutrients and xylose are gradually added.
  • the process includes growing the yeast strain in a medium including xylose and transferring the yeast strain from the medium to a feed solution.
  • Xylitol produced is recovered from the medium.
  • the feed solution comprises of xylose in water.
  • Xylitol produced in the feed solution is recovered and the yeast strain is recycled at least once.
  • the recycling comprises transferring the yeast strain to another feed solution that comprises of xylose in water.
  • the yeast strain is grown in a nutrient rich medium, in which nutrients and xylose are gradually added, which includes growing the yeast strain in a growth medium gradually supplemented by nutrients and xylose till required cell mass is achieved and xylitol is produced.
  • Xylitol produced is recovered from the medium.
  • Yeast cells so grown are separated from the medium and transferred to a feed solution of xylose in water.
  • Xylitol produced is recovered from the feed solution and the yeast strain is recycled at least once by introducing the yeast strain in a medium containing a solution of xylose in water.
  • the media used for the cell growth may be complex or chemically defined.
  • the media used for cell growth may also contain xylose such that xylitol is produced during the cell growth stage.
  • the growth medium may be a complex medium containing complex organic compounds including but not limited to peptone and yeast extract as nitrogen source. Glucose, xylitol or any other carbon source may be used separately or in combination with each other.
  • the glucose and xylose may be autoclaved separately and added to the medium.
  • the pH of the medium is preferably maintained at 6.0 and cell concentration is preferably monitored turbidometrically at 600nm.
  • the separation of the yeast cells from medium or feed solution may be carried out by any separation method including but not limited to filtration and centrifugation.
  • Xylitol may be recovered from the media or feed solution by common purification process.
  • the yeast strain used for xylitol production should have the ability to convert xylose to xylitol.
  • the yeast may be of genus Candida. More preferably the strain of the genus may be Candida tropicalis or its mutants. Most preferably the strain may be Candida tropicalis ATCC 13803.
  • xylitol is produced by the conversion of xylose in water by a yeast strain capable of converting the xylose to xylitol that is grown independently in a nutrient rich medium.
  • the yeast strain is inoculated onto an agar plate containing growth medium and allowed to grow till colonies develop. Colonies of yeast strain are then picked up from the plate, inoculated into an inoculation medium and allowed to grow for the required inoculation period. Required amount of inoculum is added to a nutrient rich medium and yeast strain allowed to grow till the required cell mass is achieved.
  • Yeast strain is then separated from the nutrient rich medium, transferred to a feed solution of xylose in water and incubated for required incubation period for the production of xylitol.
  • Xylitol is recovered from the feed solution by common purification method.
  • a process for production of xylitol is described wherein a yeast strain capable of converting the xylose to xylitol is independently grown in a nutrient rich medium and is recycled in a feed solution of xylose in water.
  • Yeast is inoculated onto an agar plate containing growth medium and allowed to grow till colonies develop.
  • Colonies of yeast are picked up from the plate, inoculated into an inoculation medium and grown for the required incubation period. Required amount of inoculum is added to the nutrient rich growth medium and incubated till the required cell mass is achieved.
  • the yeast strain is separated from the nutrient rich growth medium, and added to a feed solution of xylose in water and incubated for the required incubation period. The yeast strain is separated again, reintroduced into a feed solution and incubated for the required incubation period. These steps are repeated at least once.
  • the feed solution from each cell recycling stage is collected and xylitol is recovered by common purification process.
  • xylitol is produced by conversion of xylose in water by a yeast strain capable of converting the xylose to xylitol that is grown independently in a nutrient rich medium including xylose.
  • the yeast strain is inoculated onto an agar plate containing growth medium and allowed to grow till colonies develop. Colonies of yeast strain are then picked up from the plate, inoculated into an inoculation medium and allowed to grow for the required inoculation period.
  • Required amount of inoculum is added to a nutrient rich medium containing xylose and yeast strain allowed to grow till the required cell mass is achieved.
  • Xylitol is recovered from the medium.
  • Yeast strain is then separated from the nutrient rich medium, transferred to a feed solution of xylose in water and incubated for required incubation period for the production of xylitol.
  • Xylitol from the feed solution is recovered by common purification method.
  • a process for production of xylitol is described wherein yeast strain capable of converting the xylose to xylitol is grown in a growth medium including xylose and recycled in a solution of xylose in water.
  • yeast is inoculated onto an agar plate containing growth medium and allowed to grow till colonies develop. Colonies of yeast are picked up from the plate, inoculated into an inoculation medium and allowed to grow.
  • inoculum is added to the nutrient rich growth medium including xylose and incubated till the required cell mass is achieved and xylose is converted into xylitol.
  • the yeast strain is separated from the medium, added to a feed solution of a solution of xylose in water and incubated for the required incubation period.
  • Xylitol is recovered from the medium.
  • the yeast strain is separated again and reintroduced into a feed solution of a solution of xylose in water and incubated for the required incubation period. These steps are repeated at least once.
  • the feed solution from each stage cell recycling is collected and xylitol is recovered by common purification process.
  • xylitol is produced by conversion of xylose in water by a yeast strain capable of converting the xylose to xylitol that is independently grown in medium to which nutrients are gradually added.
  • Yeast strain is inoculated onto an agar plate containing growth medium and allowed to grow till colonies develop. Colonies of yeast are then picked up, inoculated into an inoculation medium and allowed to grow. Required amount of inoculum is added to the growth medium that is gradually supplemented with nutrients.
  • Yeast strain is allowed to grow till the required cell mass is obtained.
  • yeast strain is then separated from the growth medium, added to a feed solution of xylose in water and allowed to react for required residence time.
  • Xylitol is recovered from the feed solution by common purification process.
  • a process for production of xylitol is described wherein yeast strain capable of converting the xylose to xylitol is independently grown in a medium gradually supplemented with nutrients and recycled in a solution of xylose in water.
  • yeast cells are inoculated onto an agar plate containing growth medium and allowed to grow till colonies develop. Colonies of yeast were then picked up, inoculated into an inoculation medium and allowed to grow.
  • inoculum Required amount of inoculum is added to the growth medium that is gradually supplemented with nutrients.
  • Yeast strain is allowed to grow till the required cell mass is obtained.
  • the yeast strain is separated from the growth medium, added to a feed solution of xylose in water and incubated for the required incubation period. After the required time, yeast strain is separated again and reintroduced into a feed solution of xylose in water and incubated. These steps are repeated at least once.
  • the feed solution from each stage cell recycling is collected and xylitol is recovered by common purification process.
  • xylitol is produced by the conversion of xylose in water by a yeast strain capable of converting the xylose to xylitol that is grown in medium to which nutrients and xylose are gradually added.
  • Yeast strain is inoculated onto an agar plate containing growth medium and allowed to grow till colonies develop. Colonies of yeast are then picked up, inoculated into an inoculation medium and allowed to grow. Required amount of inoculum is added to a growth medium that is gradually supplemented with nutrients and xylose.
  • Yeast strain is allowed to grow till the required cell mass is obtained and xylose is converted to xylitol.
  • Xylitol is recovered from the growth medium.
  • the yeast strain is separated from the growth medium, added to a feed solution of xylose in water and incubated for required incubation period.
  • Xylitol is recovered from the feed solution by common purification method.
  • a process for production of xylitol is described wherein yeast strain capable of converting the xylose to xylitol is grown in a growth medium that is gradually supplemented with nutrients and xylose and recycled in a solution of xylose in water.
  • yeast strain is inoculated onto an agar plate containing growth medium and allowed to grow till colonies develop.
  • Colonies of yeast were then picked up, inoculated into an inoculation medium and allowed to grow. Required amount of inoculum is added to the growth medium that is gradually supplemented with nutrients and xylose.
  • Yeast strain is allowed to grow till the required cell mass is obtained and xylose is converted into xylitol.
  • the yeast strain is then separated from the growth medium, added to a feed solution of xylose in water and allowed to react for required residence time.
  • Xylitol is recovered from the growth medium. After the required time, cells are again separated and reintroduced into a solution of xylose in water and incubated. These steps are repeated at least once.
  • the feed solution from each stage cell recycling is collected and xylitol is recovered by common purification process.
  • the temperature for xylitol production is preferably between the range of 26 to 3O 0 C, with 30 0 C being the preferred temperature.
  • the yeast strain is agitated at a speed in the range of 150 to 250rpm with the preferred speed being 215rpm during xylitol production stage.
  • the cell recycling step is carried out at least once, preferably at least twice and most preferably three times in succession.
  • the concentration of xylose in water is in the range of lOOg/1 to 200g/l with the preferred concentration of xylose being 150g/l.
  • the cells are incubated at a temp range of 26 to 30 0 C, the preferred temperature being 30 0 C.
  • the culture is agitated at a speed in the range of 150 to 250 rpm with the preferred speed being 250rpm.
  • Xylitol is recovered from the feed solution by common purification process.
  • C. tropicalis ATCC 13803 was inoculated on YPX agar plate containing 50g/L xylose, lOg/L yeast extract, 20g/L Bacto-peptone and 15g/L agar. Yeast strain was then inoculated into an inoculation medium containing 25g/L xylose, lOg/L yeast extract, 20g/L Bacto-peptone and 25g/L glucose pH 6.0. 5% inoculum was added to the growth medium.
  • yeast strain was carried out in a medium containing lOOg/L xylose, lOg/L yeast extract, 20g/L bacto-peptone and 30g/L glucose, with pH adjusted to 6.0, at 30 0 C and 250rpm.
  • Glucose and xylose were autoclaved separately and added to the media.
  • Substrate and products were determined by HPLC equipped with Phenomenex RNM Carbohydrate Column (50 x 7.80 mm; 8 micron) and RID detector. Cell concentration was monitored turbidometrically at 600nm.
  • Xylitol production was 47.3 g/1 (with xylitol yield of 0.5 g xylitol per gram xylose) at the end of 72 h ( Figure 1 & 2).
  • C. tropicalis ATCC 13803 was inoculated on YPX agar plate containing 50g/L xylose, lOg/L yeast extract, 20g/L Bacto-peptone and 15g/L agar. Cells of the yeast were then inoculated into an inoculation medium containing 25g/L xylose, lOg/L yeast extract, 20g/L bacto-peptone and 25g/L glucose at pH 6.0. 5% inoculum was added to the growth medium.
  • Xylose and glucose were supplied at the rate of lOOg/1 at 0 h, 72 h and 144 h and 30g/l at 0 h, lOg/1 at 24 h and 5 g/1 at 72 h and 144 h respectively in the growth medium.
  • the growth medium also contained 10g/L yeast extract, 20g/L bacto-peptone and its pH was adjusted to 6.0.
  • the fermentation was carried out at a 30 0 C and 250rpm.
  • Substrate and products were determined by HPLC equipped with Phenomenex RNM Carbohydrate Column (50 x 7.80 mm; 8 micron) and RID detector. Cell concentration was monitored turbidometrically at 600nm. There was 50% conversion to xylitol in 196h.
  • the growth medium containing yeast strain from batch or fed batch culture were centrifuged at 10,000 rpm at 4°C for 15 minutes. After centrifugation strain was separated from medium by decanting the supernatant. The strain was recycled back to the flask containing xylose (100-200 g/L) in water and incubated at desired temperature (26-30 0 C) and rpm (150- 250) on the shaker. This procedure was repeated for 4 cycles and supernatant collected on each cycle were used for analysis purpose and purification of xylitol. Results with Xylose (150 g/L ) to xylitol conversion were consistent (50 - 60%). (Fig 3 and 4 and Table 2).

Landscapes

  • Organic Chemistry (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Zoology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Microbiology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Biotechnology (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Micro-Organisms Or Cultivation Processes Thereof (AREA)

Abstract

L’invention concerne un procédé de production de xylitol à partir de xylose par une souche de levure capable de convertir le xylose en xylitol. Ledit procédé comprend les étapes consistant à cultiver indépendamment la souche de levure dans un milieu; à transférer la souche de levure du milieu à une solution d’alimentation, la solution d’alimentation comprenant du xylose dans de l’eau; et à séparer le xylitol de ladite solution.
EP09722235A 2008-03-10 2009-01-09 Procédé de production de xylitol Withdrawn EP2255008A2 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IN481MU2008 2008-03-10
PCT/IN2009/000027 WO2009116066A2 (fr) 2008-03-10 2009-01-09 Procédé de production de xylitol

Publications (1)

Publication Number Publication Date
EP2255008A2 true EP2255008A2 (fr) 2010-12-01

Family

ID=41091328

Family Applications (1)

Application Number Title Priority Date Filing Date
EP09722235A Withdrawn EP2255008A2 (fr) 2008-03-10 2009-01-09 Procédé de production de xylitol

Country Status (4)

Country Link
US (1) US20110003356A1 (fr)
EP (1) EP2255008A2 (fr)
JP (1) JP2011512866A (fr)
WO (1) WO2009116066A2 (fr)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101899479B (zh) * 2010-07-02 2012-09-05 北京化工大学 利用农林废弃物制备木糖醇的生产方法
US10893509B2 (en) * 2015-02-11 2021-01-12 Qualcomm Incorporated Multiple tri-state HARQ processes
BR112018015184B1 (pt) 2016-02-19 2022-09-06 Intercontinental Great Brands Llc Processos para criar múltiplas correntes de valor a partir de fontes de biomassa
WO2018112636A1 (fr) 2016-12-21 2018-06-28 Creatus Biosciences Inc. Procédé et organisme exprimant des transporteurs de xylose de metschnikowia pour une absorption accrue du xylose
BR112019013005A2 (pt) 2016-12-21 2019-10-08 Creatus Biosciences Inc espécie de metschnikowia isolada, método para produzir xilitol, xilitol bioderivado e composição

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100528804B1 (ko) * 2003-12-08 2005-11-15 씨제이 주식회사 균체 재사용에 의한 고수율 자일리톨의 제조방법

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2009116066A2 *

Also Published As

Publication number Publication date
WO2009116066A3 (fr) 2010-01-14
JP2011512866A (ja) 2011-04-28
WO2009116066A2 (fr) 2009-09-24
US20110003356A1 (en) 2011-01-06

Similar Documents

Publication Publication Date Title
Nigam et al. Processes of fermentative production of xylitol—a sugar substitute
Saha et al. Biotechnological production of mannitol and its applications
RU2108388C1 (ru) Способ получения ксилита из водного раствора ксилозы
JP2011525357A (ja) 酵母バイオマスの製造方法
US7217545B2 (en) Method for production of lactic acid
Ravikumar et al. Microbial hosts for production of D-arabitol: current state-of-art and future prospects
EP2791348B1 (fr) Procédé de production par fermentation d'acide lactique à partir d'un extrait de plante en présence d'un sel de magnésium caustique
US20110003356A1 (en) Process for production of xylitol
US10655151B2 (en) Process for fermenting sugars containing oligomeric saccharides
Barathikannan et al. Xylitol: Production, optimization and industrial application
Rao et al. Isolation and characterization of xylitol-producing yeasts from the gut of colleopteran insects
EP1437415A1 (fr) Préparation d'acide lactique d'un substrat contenant des pentoses
Feher et al. Integrated process of arabinose biopurification and xylitol fermentation based on the diverse action of Candida boidinii
JP2000210095A (ja) キシリト―ル又はｄ―キシルロ―スの製造法
US10006059B2 (en) Selective microbial production of xylitol from biomass based sugar stream with enriched pentose component
US7083955B2 (en) Preparation of lactic acid from a pentose-containing substrate
JP4365862B2 (ja) カンジダトロピカリスｃｊ−ｆｉｄ菌株（ｋｃｔｃ１０４５７ｂｐ）およびそれを利用したキシリトールの生産方法
JP2000201690A (ja) キシリト―ルの製造法
CN102796797A (zh) 微生物转化葡萄糖制备木糖醇及其中间体d-木酮糖的方法及所用的菌种
KR101425172B1 (ko) 전분을 함유하는 바이오매스로부터 당수율을 향상시키는 방법
TW201139679A (en) Method of treating raw materials containing lignocellulose as substrate for microbial fermentation
JP2004337099A (ja) エタノールの製造方法
WO2023089629A1 (fr) Procédé de production d'érythritol à partir de ressources renouvelables
KR0180986B1 (ko) 옥수수 속대의 가수분해물질로부터 미생물 발효에 의한 자일리톨의 제조방법
Pramasari et al. Short-term Meyerozyma caribbica Y67 adaptation in sugarcane trash hemicellulosic hydrolysate for xylitol production

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20100923

AK Designated contracting states

Kind code of ref document: A2

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK TR

AX Request for extension of the european patent

Extension state: AL BA RS

17Q First examination report despatched

Effective date: 20110301

DAX Request for extension of the european patent (deleted)
STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20120801